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Compressor specification

A conveying line inlet air velocity, Ci, will need to be specified for the given material and conveying conditions, and a pipeline bore, d, will also need to be evaluated. By re-arranging the above equations and substituting for constants (including R) and free air conditions it can be shown that  [Pg.180]

This is the volumetric flow rate of air required for conveying the material through the pipeline. To this may need to be added an allowance for any leakage of air across the [Pg.180]

The air supply pressure to be specified will be pi plus allowances for any pressure drops, such as that between the compressor and the material feed point into the pipeline. [Pg.180]

It should be emphasised that absolute values of both pressure and temperature must always be used in all of the above equations. [Pg.180]


One way to decrease your reliability and cause problems is to not men tion fouling potential in centrifugal compressor specifications if proce.s.s experience exists. The experience may exist but not be recognized... [Pg.442]

Other information compressor type, material of construction, stress relief requirement, project compressor specifications, site conditions, available utilities, peimltted oil level in discharge gas, miiumum design metal ternperature (MDMT), insulation requirement, steam out condition, etc. [Pg.41]

Turbine/Compressor Specific Speed 0.3 [Pg.319]


See other pages where Compressor specification is mentioned: [Pg.156]    [Pg.441]    [Pg.450]    [Pg.451]    [Pg.453]    [Pg.355]    [Pg.356]    [Pg.384]    [Pg.384]    [Pg.478]    [Pg.583]    [Pg.681]    [Pg.681]    [Pg.766]    [Pg.177]    [Pg.307]    [Pg.682]    [Pg.686]    [Pg.778]    [Pg.739]    [Pg.739]    [Pg.743]    [Pg.743]    [Pg.683]    [Pg.683]    [Pg.764]    [Pg.681]    [Pg.681]    [Pg.685]    [Pg.685]    [Pg.588]    [Pg.588]    [Pg.649]    [Pg.316]    [Pg.353]    [Pg.180]    [Pg.330]   


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